BACKGROUND OF THE INVENTION
[0001] The present invention relates to combustion technology, especially for gas turbines.
It refers to a method for premixing air with a gaseous fuel for being burned in a
combustion chamber according to the preamble of claim 1. It further relates to a burner
arrangement for conducting such a method.
PRIOR ART
[0002] Swirl burners are devices that, by giving sufficiently strong swirl to an air flow,
lead to the formation of a central reverse flow region (Central Recirculation Zone
CRZ, vortex breakdown mechanism), which can be used for the stabilization of flames
in gas turbine combustors.
[0003] Targeting best fuel-air premixing and low pressure drop is often a challenge.
[0004] Good fuel/air premixing must be in fact achieved in a mixing region before the CRZ
where the flame is stabilized. This implies sufficiently high pressure losses in this
region, i.e. the use of a swirler with high swirl number, allowing for high velocity
tangential shearing in the fuel-air mixing section before vortex breakdown takes place.
[0005] High swirl number flows however give origin to excessive shearing at CRZ with significant
increase of pressure losses just in this region. These pressure loss characteristics
are shown in Fig. 1 from the Large Eddy Simulation of two different axial swirl burner
arrangements with swirl numbers of 0.7 and 0.56. The burner arrangement 20 of Fig.
1 (b) comprises an air tube 21 extending along burner axis 23 and opening at one end
into combustion chamber 22. A central cylindrical bluff body 27 arranged concentrically
within air tube 21 defines an annular channel for air and air/fuel flow to combustion
chamber 22, resulting in central recirculation zone 26. Fuel is introduced into the
air stream at a concentric swirl device 24 and mixed with the air in a subsequent
mixing section 25.
[0006] The high swirl number variant (open squares in Fig. 1 (a)) is characterized by a
non-dimensional pressure loss Dp (measured in units given by the dynamic head in terms
the bulk flow velocity in the mixing section) in the mixing section of approx. 2.
This can ensure good fuel/air premixing but a rather large and not necessary pressure
loss of approx. 8 at the CRZ.
[0007] The low swirl number variant (filled triangles in Fig. 1 (a)) gives instead a pressure
loss of approx. 0.7 in the mixing section which is not effective for fuel-air premixing
and acceptable pressure drop of approx. 5.5 around the CRZ.
[0008] Thus, good air/fuel premixing and low pressure loss at the beginning of the CRZ is
difficult to be put into practice at the same time with a single swirl device. Document
US 6,438,961 B2 discloses a burner for use in a combustion system of a heavy-duty industrial gas
turbine, which includes a fuel/air premixer having an air inlet, a fuel inlet, and
an annular mixing passage. The fuel/air premixer mixes fuel and air into a uniform
mixture for injection into a combustor reaction zone. The burner also includes an
inlet flow conditioner disposed at the air inlet of the fuel/air premixer for controlling
a radial and circumferential distribution of incoming air. The pattern of perforations
in the inlet flow conditioner is designed such that a uniform air flow distribution
is produced at the swirler inlet annulus in both the radial and circumference directions.
The premixer includes a swozzle assembly having a series of preferably air foil shaped
turning vanes that impart swirl to the airflow entering via the inlet flow conditioner.
Each air foil contains internal fuel flow passages that introduce natural gas fuel
into the air stream via fuel metering holes that pass through the walls of the air
foil shaped turning vanes. By injecting fuel in this manner, an aerodynamically clean
flow field is maintained throughout the premixer. By injecting fuel via two separate
passages, the fuel/air mixture strength distribution can be controlled in the radial
direction to obtain optimum radial concentration profiles for control of emissions,
lean blow outs, and combustion driven dynamic pressure activity as machine and combustor
load are varied.
[0009] Document
US 2009/056336 A1 discloses a burner for use in a combustion system of an industrial gas turbine. The
burner includes a fuel/air premixer including a splitter vane defining a first, radially
inner passage and a second, radially outer passage, the first and second passages
each having air flow turning vane portions which impart swirl to the combustion air
passing through the premixer. The vane portions in each passage are commonly configured
to impart a same swirl direction in each passage. A plurality of splitter vanes may
be provided to define three or more annular passages in the premixer.
[0010] Document
US 2010/293956 A discloses fuel nozzle auxiliary vane comprising a vane mountable base comprising
a fuel inlet, wherein the vane mountable base is configured to mount to a surface
of a main vane disposed in an airflow path of a fuel nozzle. The fuel nozzle auxiliary
vane also includes a body extending from the vane mountable base, wherein the body
comprises a fuel passage that turns from the fuel inlet to a fuel outlet, and the
fuel outlet has a fuel outlet direction generally crosswise to a fuel inlet direction
through the fuel inlet.
[0011] Document
US 7,137,258 B2 discloses a combustor including a center nozzle surrounded by a plurality of outer
nozzles, the center nozzle and each of the outer nozzles having a fuel passage and
an air passage, with a swirler surrounding the fuel passage and having a plurality
of vanes projecting radially within the air passage, each vane having a trailing edge
arranged at a swirl angle relative to a longitudinal axis of the nozzle, wherein the
swirl angle for the swirler in the center nozzle is different than the swirl angle
for the swirlers in the plurality of outer nozzles.
[0012] Document
US 7,578,130 B1 discloses methods and systems for combustion dynamics reduction. A combustion chamber
may include a first premixer and a second premixer. Each premixer may include at least
one fuel injector, at least one air inlet duct, and at least one vane pack for at
least partially mixing the air from the air inlet duct or ducts and fuel from the
fuel injector or injectors. Each vane pack may include a plurality of fuel orifices
through which at least a portion of the fuel and at least a portion of the air may
pass. The vane pack or packs of the first premixer may be positioned at a first axial
position and the vane pack or packs of the second premixer may be positioned at a
second axial position axially staggered with respect to the first axial position.
[0013] Document
EP 2 685 164 A1 discloses an axial swirler for a gas turbine burner comprising a vane ring with a
plurality of swirler vanes circumferentially distributed around a swirler axis, each
of said swirler vanes comprising a trailing edge in order to achieve a controlled
distribution of the exit flow velocity profile and/or the fuel equivalence ratio in
the radial direction, said trailing edge being discontinuous with the trailing edge
having a discontinuity at a predetermined radius.
[0014] Usually only one swirler is used for vortex breakdown and mixing. This is not optimal
because good fuel/air premixing requires high swirl but this gives origin to too high
pressure drop around the CRZ.
SUMMARY OF THE INVENTION
[0015] It is an object of the present invention to provide a premixing method and burner
arrangement, which avoid the disadvantages of known methods and devices and:
- achieve low pressure drop and, at the same time, ensure best fuel/air premixing;
- give the possibility of different discharge flow radial velocity distributions;
- spread convective time lags from fuel injection to flame for control of thermoacoustic
instabilities; and
- allow fuel staging.
[0016] This and other objects are obtained by a method according to Claim 1 and burner arrangement
according to Claim 15.
[0017] The method according to the invention for premixing air with a gaseous fuel for being
burned in a combustion chamber comprises the steps of:
guiding said air in an air stream along a burner axis through a coaxial air tube into
a combustion chamber arranged at an end of said air tube;
impressing a swirl on said air stream by passing it through a first swirl device concentrically
arranged within said air tube and comprising a plurality of radially oriented first
blades;
injecting gaseous fuel into said air stream at said first swirl device; and
mixing said air in said air stream with the injected gaseous fuel in a first mixing
zone arranged just after said first swirl device.
[0018] It is characterized in that it further comprises the steps of:
sending the mixed fuel/air stream leaving said first mixing zone through at least
one second swirl device concentrically arranged within said air tube and comprising
a plurality of radially oriented second blades to reduce the swirl of the mixed fuel/air
stream;
injecting gaseous fuel into said mixed fuel/air stream at said second swirl device;
and
further mixing said mixed fuel/air stream with the injected gaseous fuel in a second
mixing zone arranged just between said second swirl device and said combustion chamber.
[0019] According to an embodiment of the inventive method the gaseous fuel is injected at
said first and second swirl device by means of gas holes provided on the suction sides
and/or pressure sides of said first and second blades.
[0020] Especially, said gas holes are arranged in rows oriented perpendicular to the burner
axis.
[0021] According to another embodiment of the inventive method said first swirl device has
a first swirl number, said second swirl device has a second swirl number, and said
second swirl number is smaller than said first swirl number.
[0022] According to a further embodiment of the inventive method each of said first and
second swirl devices has a number of blades between 6 and 10.
[0023] According to another embodiment of the inventive method the cylindrical cross section
of the blades of the first and second swirl device has the shape of an airfoil in
order to reduce a pressure drop.
[0024] Especially, each of the blades of the first and second swirl device has a leading
edge and a trailing edge, whereby the leading edge of the blades of the second swirl
device is aligned in terms of inflow angle with outflow angle of the trailing edge
of the blades of the first swirl device.
[0025] When there are more than two swirl devices arranged in a series along the burner
axis, the leading edge of the blades of the following swirl device is aligned in terms
of inflow angle with outflow angle of the trailing edge of the blades of the foregoing
swirl device.
[0026] Specifically, said airfoils of said swirl devices are designed to produce a certain
exit flow angle α of the air/fuel flow, whereby said exit flow angle α has a predetermined
dependence α(r) of the radius r with respect to the burner axis.
[0027] More specifically, tanα(r)=H.r+K with constants H and K.
[0028] Alternatively, tanα(r) is proportional to 1/r.
[0029] Alternatively, tanα(r)= const.
[0030] According to just another embodiment of the inventive method the air is guided through
a cylindrical coaxial air tube having an inner air tube radius, in an annular space
between said coaxial air tube and a concentric central bluff body having an outer
bluff body radius, whereby the ratio between said outer bluff body radius and said
inner air tube radius is between 0.3 and 0.8.
[0031] According to another embodiment of the inventive method the fuel is supplied to the
blades of the first and second swirl device via respective cavities within said blades
by means of a fuel distribution system, which allows to control the fuel supply to
each swirl device, each blade within said swirl device, and each of said suction and
pressure sides of the blade, and combustion instabilities within said combustion chamber
are controlled by means of said fuel distribution system via fuel staging between
different swirl devices and/or different sides of the blades. According to a further
embodiment of the inventive method said first and second swirl devices have an outer
radius R and said first mixing zone has an axial length L, and said ratio L/R is between
0.5 and 4.
[0032] The inventive burner arrangement for conducting a method according to the invention
comprises an air tube extending along a burner axis and opening at one end into a
combustion chamber, a first coaxial swirl device arranged concentrically within said
air tube at a first distance from said combustion chamber, said first swirl device
comprising a plurality of radially oriented first blades and first means for injecting
fuel into an air stream passing said first swirl device.
[0033] It is characterized in that at least one second swirl device is arranged within said
air tube downstream of said first swirl device, thereby defining a first mixing section
between said first and second swirl device, whereby said second swirl device comprises
a plurality of radially oriented second blades and second means for injecting fuel
into a fuel/air stream passing said second swirl device.
[0034] An embodiment of the inventive burner arrangement is characterized in that said second
swirl device is arranged at a second distance from said combustion chamber, thereby
defining a second mixing section.
[0035] Another embodiment of the inventive burner arrangement is characterized in that said
first and second fuel injection means comprises a plurality of gas holes provided
on the suction sides and/or pressure sides of said first and second blades.
[0036] Specifically, said gas holes are arranged in rows oriented perpendicular to the burner
axis.
[0037] A further embodiment of the inventive burner arrangement is characterized in that
said first swirl device has a first swirl number, said second swirl device has a second
swirl number, and said second swirl number is smaller than said first swirl number.
[0038] Another embodiment of the inventive burner arrangement is characterized in that each
of said first and second swirl devices has a number of blades between 6 and 10.
[0039] Just another embodiment of the inventive burner arrangement is characterized in that
the cylindrical cross section of the blades of the first and second swirl device has
the shape of an airfoil.
[0040] Specifically, each of the blades of the first and second swirl device has a leading
edge and a trailing edge, whereby the leading edge of the blades of the second swirl
device is aligned in terms of inflow angle with outflow angle of the trailing edge
of the blades of the first swirl device.
[0041] When there are more than two swirl devices arranged in a series along the burner
axis, the leading edge of the blades of the following swirl device is aligned in terms
of inflow angle with outflow angle of the trailing edge of the blades of the foregoing
swirl device.
[0042] Another embodiment of the inventive burner arrangement is characterized in that said
airfoils of said swirl devices are designed to produce a certain exit flow angle α
of the air/fuel flow, whereby said exit flow angle α has a predetermined dependence
α(r) of the radius r with respect to the burner axis).
[0043] Specifically, tanα(r)=H.r+K with constants H and K.
[0044] Alternatively, tanα(r) is proportional to 1/r.
[0045] Alternatively, tanα(r)= const.
[0046] Another embodiment of the inventive burner arrangement is characterized in that the
air tube is cylindrical in shape having an inner air tube radius, that a concentric
central bluff body is arranged within said air tube having an outer bluff body radius,
and that the ratio between said outer bluff body radius and said inner air tube radius
is between 0.3 and 0.8.
[0047] A further embodiment of the inventive burner arrangement is characterized in that
the fuel is supplied to the blades of the first and second swirl device via respective
cavities within said blades by means of a fuel distribution system, which allows to
control the fuel supply to each swirl device, each blade within said swirl device,
and each of said suction and pressure sides of the blade.
[0048] Another embodiment of the inventive burner arrangement is characterized in that said
first and second swirl devices have an outer radius R and said first mixing zone has
an axial length L, and said ratio L/R is between 0.5 and 4.
BRIEF DESCRIPTION OF THE DRAWINGS
[0049] The present invention is now to be explained more closely by means of different embodiments
and with reference to the attached drawings.
- Fig. 1
- shows a known burner arrangement with one swirl device (b) and a diagram of the non-dimensional
pressure drop along the axis of said burner arrangement for two different swirl devices
with different swirl numbers (a);
- Fig. 2
- shows a burner arrangement according to an embodiment of the invention with two subsequent
swirl devices of different swirl number (b) and the resulting non-dimensional pressure
drop along the axis of said burner arrangement (a);
- Fig. 3
- shows a 3-dimensional drawing of the configuration of an exemplary swirl device with
a plurality of radial airfoil blades, which can be used in the present invention;
- Fig. 4
- shows a sectional view of a burner arrangement according to another embodiment of
the invention with two swirl devices having fuel injection means at the pressure and
suction sides of their airfoil blades;
- Fig. 5
- shows a more detailed schematics of the alignment between the blades of the first
and second swirl devices; and
- Fig. 6
- shows axial views of the first and second swirl devices with a respective fuel distribution
system (a and b), and the schematics of the fuel distribution within each airfoil
(c).
DETAILED DESCRIPTION OF DIFFERENT EMBODIMENTS OF THE INVENTION
[0050] The basic idea of the present invention relates to a series of two axial swirl burners
or devices, the first swirl device with high swirl for optimization of fuel/air mixing
and the second swirl device with low swirl for low pressure drop at the Central Recirculation
Zone (CRZ).
[0051] Thus, the invention disclosed here comprises a swirl/mixing arrangement realized
with a given number of two or more axial swirl devices arranged sequentially along
a burner axis. Fuel is injected from cavities obtained in the swirler blades. The
pressure loss characteristic in case of two sequential swirl devices is shown in a
figure similar to Fig. 1 in Fig. 2.
[0052] The burner arrangement 10 of Fig. 2 comprises an air tube 11 extending along a burner
axis 13 and opening at the downstream end into a combustion chamber 12, where a Central
Recirculation Zone (CRZ) 19 is established during operation of the burner. A central,
cylindrical and coaxial bluff body 18 within air tube 11 defines an annular channel
for air and air/fuel flow towards combustion chamber 12. Two concentric swirl devices
14 and 16 are provided in series in the annular channel, thereby defining a first
mixing section 15 between the two swirl devices 14, 16, and a second mixing section
17 between the second swirl device 16 and the entrance of combustion chamber 12. At
both swirl devices 14 and 16, gaseous fuel is injected into the passing air stream.
[0053] As can be seen from the diagram in Fig. 2(a), these characteristics (high swirl in
swirl device 14; low swirl in swirl device 16) allow for very good premixing of the
portion of fuel injected from the first swirl device 14, with the second swirl device
16 working as a de-swirl device, allowing for low pressure drop around the CRZ 19.
[0054] A second important advantage of this arrangement is the spread of convective time
lags of fuel to the flame with positive impact on combustion dynamics.
[0055] In more detail, each swirl device comprises a given number of radially extended blades
with cross section at a given radius having an airfoil shape. Fuel is injected from
holes drilled on the suction and/or pressure sides of each swirler blade. The design
allows to optimize mixing and pressure drop and, at the same time, gives flexibility
on the control of time lags between fuel injection and flame.
[0056] Thus, the basic component of the present invention is a swirl device 24, as shown
in Fig. 3, which comprises a series of radial blades 28 arranged circumferentially
around a cylindrical bluff body 27, which blades 28 are designed to impart a swirl
component to an air flow entering along burner axis 23 into air tube 21 of the mentioned
device. The device can be designed in order to target any possible radial distribution
of axial and tangential velocities, for example satisfying the inviscid conservation
equations of total pressure and radial momentum and a specific radial distribution
of exit flow angle α. The invention applies to any function describing the radial
distribution of swirler exit flow angle α.
[0057] The burner arrangement 10 according to the present invention (see Fig. 4) comprises
at least two swirl devices 14 and 16 arranged sequentially in the flow direction with
a mixing section 15 in between. The first swirl device 14 is characterized by high
swirl number while the second swirl device 16 is characterized by low swirl number.
Fuel is injected in the stream of air 33 flowing through the two swirl devices 14
and 16 from gas holes 29a,b and 30a,b placed on the suction and/or pressure sides
of the swirler blades 29 and 30. Fuel is distributed via cavities obtained within
the swirler blades 29, 30 and connected to an external fuel distribution ring organized
around the swirl devices (see Fig. 6).
[0058] The first swirl device 14 imparts a high swirl to the air stream which helps to obtain
good fuel/air mixing in the mixing section 15 (of axial length L) placed between the
two swirl devices 14 and 16. The main scope of the second swirl device 16 is instead
to reduce the swirl number (de-swirl function) before vortex breakdown takes place.
The second swirl device 16 is used also to inject a portion of the fuel in order to
have a spread of fuel time lags to the flame which helps on the side of flame dynamics.
[0059] Possible radial distributions of axial and tangential velocities of the swirler are
obtained from three types of radial distribution of blade exit flow angle α(r):
- A) whose tangent is linearly increasing in the radial direction, i.e. such that tanα(r)
= W/U = H.r+K with H and K constants and W, U tangential and axial velocities;
- B) with tanα(r) = W/U = const.; and
- C) with tanα(r) = W/U proportional to 1/r (implying irrotational flow and U=const).
[0060] Hybrid combinations of these distributions are also possible, e.g. linear increase
up to an intermediate radius, i.e. distribution A) and decrease above it, i.e. distribution
B).
[0061] Each distribution is characterized by a swirl number which is determined by the distribution
itself and the values of exit flow angle at minimum (hub) and maximum (tip) radiuses
of the blade.
[0062] Fig. 5 shows a more detailed schematic of a radial cross section of the invention
(only one blade/swirl device is shown). The leading edge of the high swirl device
(blade 29) is aligned with the main flow axis. The airfoil is designed in order to
produce an exit flow angle α
1 = 50°. The second swirl device (blade 30) must be able to produce a reduction in
exit flow angle. For this reason the second swirl device is designed counter-swirling
to the first one.
[0063] In order to avoid flow separation, the camber line of the second swirl device (blade
30) is aligned at the leading edge with the camber line of the first swirl device
(blade 29) at the trailing swirler edge. This angle is therefore reduced through the
extent of the second swirl device by a rotation of the flow θ given by α
1-α
2 with α
2 being the exit flow angle desired before vortex breakdown.
[0064] The present invention includes also a fuel distribution system (Fig. 6) characterized
by one external fuel distribution ring 31 and 32 which distributes fuel via fuel supply
lines 31 a, 32a to cavities obtained inside the swirler blades 29, 30. This fuel is
injected into the air stream from gas holes 29a,b and 30a,b drilled on the suction
and/or pressure side of the blades (see Fig. 4). The fuel supply to the swirl devices
14 and 16 via fuel supply line 34 can be independently controlled by valves V1 and
V2 (Fig. 6a and b).
[0065] The possibility of staging fuel between suction and pressure side (independent feed
of fuel to suction and pressure sides) is also included in this invention. Therefore,
the fuel supply to the gas holes of the suction and pressure side of the blades via
fuel supply line 35 can be independently controlled by valves V3 and V4 (Fig. 6c).
[0066] In summary, the invention covers a burner arrangement capable of imparting swirl
to an air stream and injecting fuel which premixes with the air stream.
[0067] In detail, there are the following characteristic features:
- The arrangement comprises a sequence of minimum 2 and maximum 4 axial swirl devices
with different swirl numbers for optimal pressure drop, fuel air premixing and combustion
dynamics;
- The number of swirler blades for each swirl device is between 6 and 10 to allow control
of fuel air premixing and homogenization of discharge flow;
- The ratio between minimum and maximum radius of the swirl devices is between 0.25
and 0.5;
- The swirl number of each single swirl device is between 0.3 and 0.8
- The cylindrical cross section of the blades is shaped like an airfoil for reduction
of pressure drop;
- A fuel/air mixing section is provided between two consecutive swirl devices with axial
extension L with ratio L/R between 0.5 and 4 (with R external radius of the swirl
devices).
- There are several distributions of exit flow angle possible, i.e. tanα(r) = W/U =
H.r+K, tanα(r) = W/U = const., and tanα(r) = W/U proportional to 1/r;
- Leading edge of blades of each swirl device is aligned in terms of inflow angle with
outflow angle of trailing edge of upstream swirl device;
- A fuel distribution system is given by an external ring pipe capable of feeding the
fuel to the blades via cavities. The possibility of staging fuel between suction and
pressure sides and between several swirl devices is advantageous;
- A method can be used to control combustion instabilities via staging fuel between
different stages (pressure-suction sides, between different swirl devices);
[0068] The advantage(s) of the present invention is:
It allows to explore a totally new burner concept with potential of good fuel/air
premixing and low pressure drop. The spread of convective time lags between fuel and
flame is a promising solution for reducing the amplitude of the flame dynamic response
(Flame Transfer Function).
LIST OF REFERENCE NUMERALS
[0069]
- 10, 20
- burner arrangement
- 11, 21
- air tube
- 12, 22
- combustion chamber
- 13, 23
- burner axis
- 14, 24
- swirl device
- 15, 25
- mixing section
- 16
- swirl device
- 17
- mixing section
- 18, 27
- bluff body
- 19, 26
- central recirculation zone (CRZ)
- 28
- blade (swirl device)
- 29, 30
- blade (swirl device)
- 29a
- gas hole (suction side)
- 29b
- gas hole (pressure side)
- 30a
- gas hole (suction side)
- 30b
- gas hole (pressure side)
- 31, 32
- fuel distribution ring
- 31 a, 32a
- fuel supply line
- 33
- air
- 34, 35
- fuel supply line
- V1-V4
- valve
1. Method for premixing air (33) with a gaseous fuel for being burned in a combustion
chamber (12), said method comprising the steps of:
guiding said air (33) in an air stream along a burner axis (13) through a coaxial
air tube (11) into a combustion chamber (12) arranged at an end of said air tube (11);
impressing a swirl on said air stream by passing it through a first swirl device (14)
concentrically arranged within said air tube (11) and comprising a plurality of radially
oriented first blades (29);
injecting gaseous fuel into said air stream at said first swirl device (14); and
mixing said air in said air stream with the injected gaseous fuel in a first mixing
zone (15) arranged just after said first swirl device (29);
characterized in that it further comprises the steps of
sending the mixed fuel/air stream leaving said first mixing zone (15) through at least
one second swirl device (16) concentrically arranged within said air tube (11) and
comprising a plurality of radially oriented second blades (30) to reduce the swirl
of the mixed fuel/air stream;
injecting gaseous fuel into said mixed fuel/air stream at said second swirl device
(16); and
further mixing said mixed fuel/air stream with the injected gaseous fuel in a second
mixing zone (17) arranged just between said second swirl device (30) and said combustion
chamber (19).
2. Method as claimed in Claim 1, characterized in that the gaseous fuel is injected at said first and second swirl device (14, 16) by means
of gas holes (29a,b; 30a,b) provided on the suction sides and/or pressure sides of
said first and second blades (29, 30).
3. Method as claimed in Claim 2, characterized in that said gas holes (29a,b; 30a,b) are arranged in rows oriented perpendicular to the
burner axis (13)
4. Method as claimed in Claim 1, characterized in that said first swirl device (14) has a first swirl number, said second swirl device (16)
has a second swirl number, and said second swirl number is smaller than said first
swirl number.
5. Method as claimed in Claim 1, characterized in that each of said first and second swirl devices (14, 16) has a number of blades (29,
30) between 6 and 10.
6. Method as claimed in Claim 1, characterized in that the cylindrical cross section of the blades (29, 30) of the first and second swirl
device (14, 16) has the shape of an airfoil in order to reduce a pressure drop.
7. Method as claimed in Claim 6, characterized in that each of the blades (29, 30) of the first and second swirl device (14, 16) has a leading
edge and a trailing edge, whereby the leading edge of the blades (30) of the second
swirl device (16) is aligned in terms of inflow angle with outflow angle of the trailing
edge of the blades (29) of the first swirl device (14).
8. Method as claimed in Claim 6, characterized in that said airfoils of said swirl devices (14, 16) are designed to produce a certain exit
flow angle α of the air/fuel flow, whereby said exit flow angle α has a predetermined
dependence α(r) of the radius r with respect to the burner axis (13).
9. Method as claimed in Claim 7, characterized in that tanα(r)=H.r+K with constants H and K.
10. Method as claimed in Claim 7, characterized in that tanα(r) is proportional to 1/r.
11. Method as claimed in Claim 7, characterized in that tanα(r)= const.
12. Method as claimed in Claim 1, characterized in that the air (33) is guided through a cylindrical coaxial air tube (11) having an inner
air tube radius, in an annular space between said coaxial air tube (11) and a concentric
central bluff body (18) having an outer bluff body radius, whereby the ratio between
said outer bluff body radius and said inner air tube radius is between 0.3 and 0.8.
13. Method as claimed in Claim 2, characterized in that the fuel is supplied to the blades (29, 30) of the first and second swirl device
(14, 16) via respective cavities within said blades (29, 30) by means of a fuel distribution
system (34, 35, V1-V4), which allows to control the fuel supply to each swirl device
(14, 16), each blade (29, 30) within said swirl device (14, 16), and each of said
suction and pressure sides of the blade (29, 30), and that combustion instabilities
within said combustion chamber (12) are controlled by means of said fuel distribution
system (34, 35, V1-V4) via fuel staging between different swirl devices (14, 16) and/or
different sides of the blades (29, 30).
14. Method as claimed in Claim 1, characterized in that said first and second swirl devices (14, 16) have an outer radius R and said first
mixing zone (15) has an axial length L, and said ratio L/R is between 0.5 and 4.
15. Burner arrangement for conducting a method according to claim 1, comprising an air
tube (11) extending along a burner axis (13) and opening at one end into a combustion
chamber (12), a first coaxial swirl device (14) arranged concentrically within said
air tube (11) at a first distance from said combustion chamber (12), said first swirl
device (14) comprising a plurality of radially oriented first blades (29) and first
means (29a,b) for injecting fuel into an air stream passing said first swirl device
(14), characterized in that at least one second swirl device (16) is arranged within said air tube (11) downstream
of said first swirl device (14), thereby defining a first mixing section (15) between
said first and second swirl device (14, 16), whereby said second swirl device (16)
comprises a plurality of radially oriented second blades (30) and second means (30a,b)
for injecting fuel into a fuel/air stream passing said second swirl device (16).
16. Burner arrangement as claimed in Claim 15, characterized in that said second swirl device (16) is arranged at a second distance from said combustion
chamber (12), thereby defining a second mixing section (17).
17. Burner arrangement as claimed in Claim 15, characterized in that said first and second fuel injection means comprises a plurality of gas holes (29a,b;
30a,b) provided on the suction sides and/or pressure sides of said first and second
blades (29, 30).
18. Burner arrangement as claimed in Claim 17, characterized in that said gas holes (29a,b; 30a,b) are arranged in rows oriented perpendicular to the
burner axis (13).
19. Burner arrangement as claimed in Claim 15, characterized in that said first swirl device (14) has a first swirl number, said second swirl device (16)
has a second swirl number, and said second swirl number is smaller than said first
swirl number.
20. Burner arrangement as claimed in Claim 15, characterized in that each of said first and second swirl devices (14, 16) has a number of blades (29,
30) between 6 and 10.
21. Burner arrangement as claimed in Claim 15, characterized in that the cylindrical cross section of the blades (29, 30) of the first and second swirl
device (14, 16) has the shape of an airfoil.
22. Burner arrangement as claimed in Claim 21, characterized in that each of the blades (29, 30) of the first and second swirl device (14, 16) has a leading
edge and a trailing edge, whereby the leading edge of the blades (30) of the second
swirl device (16) is aligned in terms of inflow angle with outflow angle of the trailing
edge of the blades (29) of the first swirl device (14).
23. Burner arrangement as claimed in Claim 21, characterized in that said airfoils of said swirl devices (14, 16) are designed to produce a certain exit
flow angle α of the air/fuel flow, whereby said exit flow angle α has a predetermined
dependence α(r) of the radius r with respect to the burner axis (13).
24. Burner arrangement as claimed in Claim 23, characterized in that tanα(r)=H.r+K with constants H and K.
25. Burner arrangement as claimed in Claim 23, characterized in that tanα(r) is proportional to 1/r.
26. Burner arrangement as claimed in Claim 23, characterized in that tanα(r)= const.
27. Burner arrangement as claimed in Claim 15, characterized in that the air tube (11) is cylindrical in shape having an inner air tube radius, that a
concentric central bluff body (18) is arranged within said air tube (11) having an
outer bluff body radius, and that the ratio between said outer bluff body radius and
said inner air tube radius is between 0.3 and 0.8.
28. Burner arrangement as claimed in Claim 17, characterized in that the fuel is supplied to the blades (29, 30) of the first and second swirl device
(14, 16) via respective cavities within said blades (29, 30) by means of a fuel distribution
system (34, 35, V1-V4), which allows to control the fuel supply to each swirl device
(14, 16), each blade (29, 30) within said swirl device (14, 16), and each of said
suction and pressure sides of the blade (29, 30).
29. Burner arrangement as claimed in Claim 23, characterized in that said first and second swirl devices (14, 16) have an outer radius R and said first
mixing zone (15) has an axial length L, and said ratio L/R is between 0.5 and 4.